Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L95/00—Compositions of bituminous materials, e.g. asphalt, tar, pitch
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F297/00—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer
  • C08F297/02—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the anionic type
  • C08F297/04—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the anionic type polymerising vinyl aromatic monomers and conjugated dienes
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F297/00—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer
  • C08F297/02—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the anionic type
  • C08F297/04—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the anionic type polymerising vinyl aromatic monomers and conjugated dienes
  • C08F297/044—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the anionic type polymerising vinyl aromatic monomers and conjugated dienes using a coupling agent
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J3/00—Processes of treating or compounding macromolecular substances
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L53/00—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
  • C08L53/02—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers of vinyl-aromatic monomers and conjugated dienes
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L2555/00—Characteristics of bituminous mixtures
  • C08L2555/20—Mixtures of bitumen and aggregate defined by their production temperatures, e.g. production of asphalt for road or pavement applications
  • C08L2555/22—Asphalt produced above 140°C, e.g. hot melt asphalt
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L2555/00—Characteristics of bituminous mixtures
  • C08L2555/40—Mixtures based upon bitumen or asphalt containing functional additives
  • C08L2555/80—Macromolecular constituents
  • C08L2555/84—Polymers comprising styrene, e.g., polystyrene, styrene-diene copolymers or styrene-butadiene-styrene copolymers

Definitions

• the present invention relates to a process for preparing a polymer modified bituminous binder composition that has improved ductility, particularly at low temperatures, and is suitable for hot mix asphalt paving applications in the substantial absence of crosslinking agents.
• the present invention further relates to a polymer modified bituminous binder composition having improved ductility, particularly at low temperatures, comprising a bitumen component and a block copolymer composition that contains one or more block copolymers having at least one monovinylaromatic block and either (I) at least one polybutadiene block having a vinyl content of less than 15 mol percent and at least one polybutadiene block having a vinyl content of greater than 25 mol percent or (II) at least one polybutadiene block having a vinyl content that tapers from a vinyl content of less than 15 mol percent at the first end adjacent to the monovinylaromatic block to a vinyl content that is greater than 25 mol percent at the second end which is furthest from the monovinylaromatic block.
• Polymer modified asphalt for paving applications and methods for preparing various polymer modified asphalt compositions are well known in the art.
• Various polymers including diene elastomers such as polybutadiene, EPDM, EPR and styrenic block copolymers (SBCs) such as styrene-butadiene-styrene (SBS) and styrene-isoprene-styrene (SIS) block copolymers, are commonly combined with bitumen to improve the performance of the bitumen. See, for example, U.S. Pat. No. 5,190,998 and U.S. Pat. No. 6,150,439.
• U.S. patent application Ser. No. 11/598,511 published as US 2007/0112102 A1 discloses a process for preparing a polymer modified bituminous binder composition in the substantial absence of crosslinking agents, using a block copolymer composition that contains a high vinyl content diblock copolymer and optionally a high vinyl content block copolymer selected from linear triblock copolymers, multiarm coupled block copolymers and mixtures thereof.
• Using such a process and composition results in a product that is storage stable, readily mixable and has a quick cure while at the same time minimizing the environmental impact caused by the addition of sulfur or sulfur-containing crosslinking agents.
• the present invention provides a way to produce polymer modified bituminous binder compositions for road/paving applications that has high ductility without the necessity of adding crosslinking agents.
• block copolymer composition of the present invention in the process of the present invention, it is possible to minimize environmental and safety concerns associated with the use of sulfur containing crosslinking agents while at the same time providing a product which demonstrates improved ductility, especially in low temperature environments.
• the present invention provides a process for preparing a polymer modified bituminous binder composition in the substantial absence of crosslinking agents that has improved ductility by:
• the block copolymer composition of the present invention comprises:
• a block copolymer of the formula S-B1-B2 wherein S is a monovinylaromatic hydrocarbon block having a peak molecular weight from about 10,000 to about 25,000, B1 is a polybutadiene block having a vinyl content of less than 15 mol percent, B2 is a polybutadiene block having a vinyl content of greater than 25 mol percent, and the ratio of B1 to B2 is greater than or equal to 1:1, and wherein the S-B1-B2 block copolymer has a peak molecular weight from about 40,000 to about 200,000; and
• each S is a monovinylaromatic hydrocarbon block having a peak molecular weight from about 10,000 to about 25,000
• each B1 is a polybutadiene block having a vinyl content of less than 15 mol percent
• each B2 is a polybutadiene block having a vinyl content of greater than 25 mol percent
• n is an integer from 2 to 6
• X is the residue of a coupling agent, the ratio of B1 to B2 is greater than or equal to 1:1
• the (S-B1-B2) n X block copolymer has a peak molecular weight that is from 1.5 to 6.0 times the peak molecular weight of the S-B1-B2 block copolymer; and wherein when both S-B1-B2 and (S-B1-B2) n X are present in the block copolymer composition, the ratio of S-B1-B2 to (S-B1-B2) n X are present in the block copolymer composition, the ratio of S-B
• the block copolymers would contain an optional polybutadiene block adjacent to the B2 block such that the formulas represented in sections (i) and (ii) above would respectively be S-B1-B2-B3 and (S-B1-B2-B3)nX wherein each B1 and B2 is as defined hereinbefore and each B3 is a polybutadiene block having a vinyl content of less than 15 mol percent.
• the peak molecular weight of the B3 block would range from about 1,000 to about 25,000 and the overall peak molecular weights of the block copolymers would be within the same range as defined hereinbefore.
• the block copolymer composition of the present invention comprises:
• S is a monovinylaromatic hydrocarbon block having a peak molecular weight from about 10,000 to about 25,000
• B4 is a polybutadiene block having a vinyl content that tapers from less than 15 mol percent at the first end adjacent to the monovinylaromatic block (S) to a vinyl content that is greater than 25 mol percent at the second end which is furthest from the monovinylaromatic block (S) and wherein the S-B4 block copolymer has a peak molecular weight from about 40,000 to about 200,000;
• each S is a monovinylaromatic hydrocarbon block having a peak molecular weight from about 10,000 to about 25,000 and each B4 is a polybutadiene block having a vinyl content that tapers from less than 15 mol percent at the first end adjacent to the monovinylaromatic block (S) to a vinyl content that is greater than 25 mol percent at the second end which is furthest from the monovinylaromatic block (S), n is an integer from 2 to 6, and X is the residue of a coupling agent and wherein the (S-B4) n X block copolymer has a peak molecular weight that is from 1.5 to 6.0 times the peak molecular weight of the S-B4 block copolymer; and
• the block copolymers would contain an optional polybutadiene block such that the formulas represented in sections (i) and (ii) above would respectively be S-B4-B5 and (S-B4-B5)nX wherein each B4 is as defined hereinbefore and each B5 is a polybutadiene block having a vinyl content of less than 15 mol percent.
• the peak molecular weight of the B5 block would range from about 1,000 to about 25,000 and the overall peak molecular weights of the block copolymers would be within the same range as defined hereinbefore.
• block copolymer composition of the present invention may still further comprise one or more additional block copolymers.
• the present invention also provides an alternative process which comprises the steps of:
• bitumen component and block copolymer composition (c) raising the temperature of the bitumen component and block copolymer composition to from about 160° C. to about 221° C. while stirring the bitumen component and block copolymer composition thereby forming a homogeneous mixture of the bitumen component and the block copolymer composition;
• this additional process may further comprise the step of diluting the homogeneous mixture to a lesser concentration either during or after the curing of the polymer modified bituminous binder composition.
• the present invention even further relates to a specific class of bituminous binder compositions and bituminous binder concentrates which comprise a bitumen component and one of the block copolymer compositions as defined hereinbefore as well as the specific block copolymer compositions utilized.
• the process of the present invention is particularly useful for preparing polymer modified bituminous binder compositions to be used for road/paving applications in areas that experience cold to severe winters since the bituminous binder compositions of the present invention have improved ductility and do not need the addition of sulfur containing crosslinking agents.
• the process of the present invention which does not require the use of crosslinking agents, it is possible to prepare polymer modified bituminous binder compositions that not only demonstrate ductility properties that are as good, if not better, than the prior art polymer modified bituminous binder compositions, especially with regard to ductility at low temperatures, but which are also safer and more environmentally friendly due to the elimination of the crosslinking agents.
• the polymer modified bituminous binder compositions of the present invention also exhibit excellent processability and cure time, as well as a reduction in phase separation.
• a bitumen component is heated in a stirred tank to a temperature from about 160° C. to about 221° C.
• the bitumen component utilized in the process according to the present invention may be any naturally occurring bitumen or it may be derived from petroleum.
• petroleum pitches obtained by a cracking process and coal tar can be used as the bitumen component as well as blends of various bitumen materials.
• suitable components include, but are not limited to, distillation or “straight-run bitumens”, precipitation bitumens (e.g. propane bitumens), blown bitumens (e.g. catalytically blown bitumen), multigrades, and mixtures thereof.
• bitumen components include, but are not limited to, mixtures of one or more of these bitumens with extenders (fluxes) such as petroleum extracts, e.g. aromatic extracts, distillates or residues, or with oils.
• extenders such as petroleum extracts, e.g. aromatic extracts, distillates or residues, or with oils.
• Suitable bitumen components are those having a penetration of in the range of from about 25 to about 400 units at 25° C.; therefore quite hard bitumens of a penetration of from about 60 to about 70 units may be used, but generally a straight run or distilled bitumen having a penetration from about 110 to about 250 units will be the most convenient to use. Both compatible as well as incompatible bitumens may be used.
• any known tank or vessel utilized in the preparation of bitumen compositions can be used provided that such tank or vessel has stirring (agitation) and heating capabilities.
• the phrase “stirred tank” refers to such tanks and vessels that have stirring (agitation) and heating means. Suitable stirring or agitation includes, but is not limited to, vertical impellers, side-arm impellers and pump around circulation.
• the bitumen component is typically placed in the stirred tank and gradually heated to a temperature in the range of from about 160° C.
• bitumen component is typically stirred or agitated during this heating phase. While the presence of air is not detrimental to the process of the present invention (i.e., the use of an open air vessel which results in the surface of the mixture coming in contact with air), the intentional introduction of air (as in the case of air curing or blown bitumen) is not necessary to the process of the present invention and is in fact discouraged since such addition would most likely result in the hardening of the bitumen component.
• the block copolymer composition (described below) is added while the bitumen component is being stirred in order to form a homogeneous mixture of the bitumen component and the block copolymer composition.
• block copolymer compositions in the form of powders, porous pellets, and/or crumb may be added all at once or divided into small amounts or batches and added at intervals over a brief period of time (e.g., over a period of 5 to 60 minutes although slightly shorter or longer times are also envisioned). In most instances, the block copolymer composition is added in the form of a porous pellet all at once. Addition of the block copolymer composition over an even longer period of time is also possible but not necessarily desirable from an economic standpoint.
• the mixture is stirred and the temperature to which the bitumen component was heated (from about 160° C. to about 221° C.) is maintained.
• the block copolymer composition may dissolve and form a homogeneous blend with simple stirring or other agitation means as noted above.
• the bitumen forms a thin film on the aggregate that is present. It is generally accepted that the thickness of this film is on the order of approximately ten microns.
• Bitumen additives are generally considered to be homogeneous within a blend if they completely disperse in the bitumen on an equal or finer scale than the film of bitumen on aggregate.
• SBS polymers dispersed in bitumen to form a phase structure comprising a polymer rich phase and a bitumen rich phase.
• the phrase “homogeneous blend” refers to a mixture that comprises the bitumen component and block copolymer composition such that the block copolymer composition is dispersed within the bitumen component on the approximate ten micron scale or less.
• a high shear mill may be utilized for the entire process, it is typically utilized for a sufficient period of time for the block copolymer to form a homogeneous blend with the bitumen component.
• the time to form a homogeneous blend utilizing high shear mixing/stirring will typically range from about 0 hours to about 8.0 hours, more typically from about 0.5 to about 4 hours and even more preferably from about 0.5 hours to about 2.0 hours.
• the stirring is typically accomplished utilizing low shear blending.
• the initial stirring is accomplished at high shear with the stirring thereafter (step (c)) being carried out at low shear.
• the stirring is continued for a period of time from about 2 to about 30 hours at a temperature that is from about 180° C. to about 221° C. in order to allow for complete curing of the mixture prior to use.
• the temperature will be from about 180° C. to about 210° C., more preferably from about 185° C. to about 199° C., and even more preferably from about 185° C. to about 195° C.
• the stirring in this step occurs for periods of time from 4 to 26 hours, preferably from 5 to 24 hours and more preferably from 5 to 15 hours and most preferably from 6 to 10 hours.
• the duration of the stirring should be decreased since there could be degradation of the polymer at temperatures higher than 199° C. when heated at this temperature for greater than 15 hours. Accordingly, when the temperature is greater than 199° C., the stirring in step (c) will last for a total period from 2 to 15 hours.
• the quantity of block copolymer composition to be added in the process of the present invention can vary based on whether it is desirable to have a concentrate which will be subsequently diluted (“let down”) before further use or whether the amount added provides the final dilution to be used at that time (the final product). Accordingly, the amount to be added will be such that the amount of block copolymer composition added to the bitumen component will be from as little as about 2% by weight to as high as about 36% by weight, based on the weight of the polymer modified bituminous binder composition.
• bituminous binder concentrate which will contain from about 6% by weight to about 36% by weight, preferably from about 9 to 30%, and more preferably from about 12% by weight to about 22% by weight, block copolymer composition (based on the total weight of the polymer modified bitumen binder composition).
• bituminous binder concentrate will at some point be diluted with more bitumen to achieve the desired final concentration for final use (typically from about 2% by weight to about 6% by weight based on the total weight of the polymer modified bitumen binder composition).
• the process of diluting a polymer modified bituminous binder concentrate to the desired concentration for use is well known in the art as a cost effective method of utilizing blending equipment.
• the bituminous binder concentrate of the present invention may be diluted (“let down”) to the final concentration during or immediately following the curing process or, in the alternative, it may be stored and/or shipped to a different location where it will later be diluted (“let down”) to the final concentration.
• the process of the present invention may optionally contain further steps in the production of polymer modified bituminous binder compositions.
• One such embodiment allows for the preparation of a concentrate comprising 6 to 36% by weight of the block copolymer composition followed by the dilution of the concentrate with more bitumen to achieve the desired final concentration (preferably for a final concentration of from about 2% by weight to about 6% by weight).
• This dilution may occur either during curing (step (c)) or subsequent to curing after step (c) provided that the temperature is maintained for the required time to achieve the cure.
• the composition maybe shipped to a different location provided that adequate temperature and agitation are maintained.
• the composition When diluting during the cure, the composition may be diluted as soon as the concentrate blend becomes homogeneous (at the beginning of step (c) or as the composition cures (during step (c)).
• This embodiment is advantageous when expensive milling equipment is used so that higher throughput may be achieved.
• the concentrate composition may be let down after the curing process is complete. This embodiment is advantageous for long term storage as the diluting bitumen may be introduced at a much lower temperature resulting in a final blend at a temperature more suitable for long term storage.
• the block copolymer composition will preferably be present in an amount from about 2% by weight to about 6% by weight, and most preferably from about 2.5% by weight to about 5% by weight, based on the total weight of the polymer modified bituminous binder composition.
• the present invention further provides for an alternative to the above process that differs from the above process in that the bitumen is first heated to a molten state, the block copolymer composition is added, and then the temperature is raised to the level for curing, from about 180° C. to about 221° C.
• the present alternative only includes changes in the process steps themselves, not within the types of materials utilized (e.g., bitumen and block copolymer composition) or means of accomplishing the steps (e.g., type of equipment utilized). More specifically, in this alternative, the bitumen component, as described hereinbefore, is heated in a stirred tank until the bitumen component is in a molten state.
• the phrase “molten state” refers to the point at which the bitumen component becomes liquid. Those skilled in the art will recognize that most bitumens reach a “molten state” within the temperature range of from about 87° C. to about 121° C., more specifically from about 93° C. to about 105° C. During this phase, the bitumen component is optionally stirred. Once the bitumen component reaches a molten state, the block copolymer composition can be added in the manner described hereinbefore. Note that while the polymer can be added at this temperature, typically the preference is to heat the bitumen to a temperature of at least 160° C. when the block copolymer is added.
• the temperature is raised to from about 180° C. to about 221° C., alternatively from about 180° C. to about 210° C., still alternatively, from about 185° C. to about 199° C., and in still another alternative, from about 185° C. to about 195° C. (as described hereinbefore) while actively stirring the bitumen component and block copolymer composition in order to form a homogeneous mixture of the two components.
• This mixture will continue to be stirred at the noted temperature for a total of from about 2 hours to about 30 hours as described hereinbefore until a cured polymer modified bituminous binder composition is obtained.
• the homogeneous mixture will be further let down as described hereinbefore either during or after the curing of the polymer modified bituminous binder composition.
• the temperature at which the mixture is stirred is greater than 199° C., preferably the mixture will be stirred for a total period of from 2 to 15 hours in order to minimize any degradation of the polymer that might occur. For temperatures less than 199° C. the time for stirring may be extended up to 30 hours.
• compositions having block copolymers that have a low vinyl block followed by a high vinyl block, as well as a high quantity (>50%) of S-B1-B2 block copolymer, or alternatively compositions having block copolymers that have a block that tapers from low vinyl to high vinyl, as well as a high quantity (>50%) of S-B4 block copolymer it is possible to achieve a product that exhibits improved ductility, particularly at low temperatures, without the need for the addition of crosslinking agents in the preparation of the polymer modified bitumen. Accordingly, with the present invention it is possible to produce a polymer modified bituminous binder composition or a bituminous binder concentrate having high ductility in the substantial absence of crosslinking agents.
• the phrase “in the substantial absence of crosslinking agents” means that the addition of crosslinking or curing agents during the preparation process is not required.
• the phrase “substantially free of crosslinking agents” means that no substantial amount of crosslinking agent is present in the product.
• traces of such crosslinking or curing agents may be present due to the active addition of insubstantial amounts of crosslinking or curing agent or residual amounts from another source such as with the addition of ground rubber and/or what naturally occurs in the bitumen.
• bituminous binder composition typically less than about 0.01% of the total weight of the polymer modified bituminous binder composition or bituminous binder concentrate.
• bituminous binder concentrate typically less than about 0.01% of the total weight of the polymer modified bituminous binder composition or bituminous binder concentrate.
• the resulting blend also demonstrates storage stable (it does not separate) and good conventional properties.
• block copolymer compositions There are two embodiments of block copolymer compositions that can be used in the above noted processes of the present invention to achieve the desired results noted. The first of these embodiments is described in more specific detail in paragraphs [0028] to [0039] and the second of these embodiments is described in more specific detail in paragraphs [0040] to [0047].
• the two embodiments are similar in that both comprise one or more block copolymers that have at least one monovinylaromatic block and a polybutadiene structure (that may either be in the form of one individual block or two different blocks) wherein the polybutadiene structure has a vinyl content such that at one end of the polybutadiene structure (the end adjacent to the monovinylaromatic block) is less than 15 mol percent and the vinyl content at the other end of the polybutadiene structure (the end furthest away from the monovinylaromatic block) is greater than 25 mol percent.
• the vinyl content in the polybutadiene structure (regardless of whether it is a one block or two block structure) is considered to taper from a low vinyl content ( ⁇ 15 mol percent) to a higher vinyl content (>25 mol percent).
• This can be accomplished either by synthesizing discrete polybutadiene blocks of low vinyl content and higher vinyl content or by continuously tapering the vinyl content from low to high in one block. It will be appreciated that a combination of these two procedures will accomplish essentially the same end result.
• the first of these embodiments comprises one or more block copolymers having at least one monovinylaromatic block, at least one polybutadiene block having a vinyl content of less than 15 mol percent and at least one polybutadiene block having a vinyl content greater than 25 mol percent. More specifically, the block copolymer compositions of this embodiment utilized in the present invention comprise:
• a block copolymer of the formula S-B1-B2 wherein S is a monovinylaromatic hydrocarbon block having a peak molecular weight from about 10,000 to about 25,000, B1 is a polybutadiene block having a vinyl content of less than 15 mol percent, B2 is a polybutadiene block having a vinyl content of greater than 25 mol percent, the ratio of B1 to B2 is greater than or equal to 1:1, and wherein the S-B1-B2 block copolymer has a peak molecular weight from about 40,000 to about 200,000; and
• each S is a monovinylaromatic hydrocarbon block having a peak molecular weight from about 10,000 to about 25,000
• each B1 is a polybutadiene block having a vinyl content of less than 15 mol percent
• each B2 is a polybutadiene block having a vinyl content of greater than 25 mol percent
• n is an integer from 2 to 6
• X is the residue of a coupling agent
• the ratio of B1 to B2 is greater than or equal to 1:1
• the (S-B1-B2) n X block copolymer has a peak molecular weight from 1.5 to 6.0 times the peak molecular weight of the S-B1-B2 block copolymer, and wherein when both S-B1-B2 and (S-B1-B2)nX are present in the block copolymer composition, the ratio of S-B1-B2 to (S-B1-B2)
• the monovinylaromatic hydrocarbon blocks in S-B1-B2 or (S-B1-B2)nX may be any monovinylaromatic hydrocarbon known for use in the preparation of block copolymers such as styrene, o-methylstyrene, p-methylstyrene, p-tert-butylstyrene, 2,4-dimethylstyrene, alpha-methylstyrene, vinylnaphthalene, vinyltoluene and vinylxylene or mixtures thereof
• the most preferred monovinylaromatic hydrocarbon for use in the polymers to be used in the process of the present invention is styrene, which is used as a substantially pure monomer or as a major component in mixtures with minor proportions of other structurally related vinyl aromatic monomer(s) such as o-methylstyrene, p-methylstyrene, p-tert-butylstyrene, 2,4-di
• the polybutadiene blocks of the above-noted formulas is a polybutadiene monomer that is a substantially pure monomer or contains minor proportions, up to 10% by weight, of structurally related conjugated dienes.
• the polybutadiene is pure.
• the term “molecular weights” refers to the true molecular weight in g/mol of the polymer or block of the copolymer.
• the molecular weights referred to in this specification and claims can be measured with gel permeation chromatography (GPC) using polystyrene calibration standards, such as is done according to ASTM 3536.
• GPC gel permeation chromatography
• polystyrene calibration standards such as is done according to ASTM 3536.
• GPC is a well-known method wherein polymers are separated according to molecular size, the largest molecule eluting first.
• the chromatograph is calibrated using commercially available polystyrene molecular weight standards.
• the molecular weight of polymers measured using GPC so calibrated are styrene equivalent molecular weights.
• the styrene equivalent molecular weight may be converted to true molecular weight when the styrene content of the polymer and the vinyl content of the diene blocks are known.
• the detector used is preferably a combination ultraviolet and refractive index detector.
• the molecular weights expressed herein are measured at the peak of the GPC trace, converted to true molecular weights, and are commonly referred to as “peak molecular weights”.
• each monovinylaromatic hydrocarbon block is from about 10,000 to about 25,000, preferably from about 12,000 to about 20,000. In an alternative embodiment, the peak molecular weight is from about 14,000 to about 18,000.
• Each block copolymer of the formula S-B1-B2 utilized in the process of the present invention will have a peak molecular weight from about 40,000 to about 200,000, preferably from about 65,000 to about 160,000, even more preferably from about 75,000 to about 150,000, and still more preferably from about 75,000 to less than 130,000.
• the peak molecular weight of the coupled block copolymers of the formula (S-B1-B2)nX is dependent upon the peak molecular weight of the block copolymer of the formula S-B1-B2 utilized.
• the peak molecular weight of the (S-B1-B2)nX block copolymers will range from about 1.5 to about 6.0 times the peak molecular weight of the S-B1-B2 block copolymer.
• the peak molecular weight of the (S-B1-B2)nX block copolymers will range from about 1.8 to about 5.0 times the peak molecular weight of the S-B1-B2 block copolymer.
• the combined molecular weight of the two butadiene blocks (B1 and B2) will range from about 25,000 to about 190,000. With regard to the two butadiene blocks (B1 and B2), they will be present at a weight ratio to one another of greater than or equal to 1:1. In other words, B1 will be present in an amount (weight percent) greater than or equal to 50% of the total of the B1-B2 segment and B2 will be present in an amount (weight percent) of less than or equal to 50% of the total of the B1-B2 segment.
• vinyl content has been used to describe the polymer product that is made when 1,3-butadiene is polymerized via a 1,2-addition mechanism. The result is a monosubstituted olefin group pendant to the polymer backbone, a vinyl group.
• the polybutadiene is present in blocks or segments which contain differing vinyl contents. It is believed that the combination of these “segments” differing in vinyl content that gives the improved ductility of the final product while still exhibiting other desirable properties for polymer modified bitumens.
• the vinyl content in the B1 block should be such that from about 5 mol percent to about 15 mol percent of the condensed polybutadiene units have a 1,2-addition configuration. Taking into consideration known anionic polymerization of butadiene processes, typically from about 7 to about 15 mol percent of the polybutadiene units will have 1,2-addition configuration.
• the vinyl content in the B2 block will be from about 25 mol percent to about 80 mol percent of the condensed polybutadiene units having a 1,2-addition configuration, more preferably from about 40 mol percent to about 75 mol percent of the condensed polybutadiene units having a 1,2-addition configuration, and even more preferably from about 50 to about 65 mol percent of the polybutadiene units having a 1,2-addition configuration.
• the monovinylaromatic hydrocarbon content of the copolymers is suitably from about 10 to about 40% by weight, based on the total block copolymer.
• the content of monovinylaromatic hydrocarbon of the copolymers will be from about 18 to about 35% by weight, more preferably from about 19 to about 32% by weight, based on the total weight of the copolymer.
• the block copolymer composition comprises a block copolymer of the formula S-B1-B2 alone.
• S is a monovinylaromatic hydrocarbon block
• B1 is a polybutadiene block having a vinyl content of less than 15 mol percent
• B2 is a polybutadiene block having a vinyl content of greater than 25 mol percent.
• S-B1-B2 may be used in combination with a coupled block copolymer of the formula (S-B1-B2)nX wherein each S is a monovinylaromatic hydrocarbon block, each B1 is a polybutadiene block having a vinyl content less than 15 mol percent, each B2 is a polybutadiene block having a vinyl content greater than 25, n is an integer from 2 to 6 and X is the residue of a coupling agent.
• n will be an integer ranging from 2 to 6.
• n will be an integer from 2 to 4, with 2 being the most preferred.
• the block copolymers of the present invention are in substantially unhydrogenated form.
• the ratio of the S-B1-B2 block copolymer to (S-B1-B2)nX block copolymer will be greater than about 1:1, preferably equal to or greater than about 3:2. In a particularly preferred embodiment, the ratio will be from about 3:2 to about 10:1 with the most preferred ratio being from about 4:1 to about 7:3.
• the block copolymer composition comprises a mixture of S-B1-B2 and (S-B1-B2)nX
• coupled polymer will always be present in an amount less than that of the S-B1-B2 block copolymer (e.g., the coupled block copolymer will be present in the composition in an amount of at most 49.9% by weight, preferably at most 40% by weight).
• this block copolymers of the present embodiment may further comprise an additional polybutadiene block (B3) having a vinyl content that is less than 15 mol percent.
• the vinyl content in the B3 block when present, will preferably be such that from about 5 mol percent to about 15 mol percent of the condensed polybutadiene units will have a 1,2-addition configuration, preferably from about 7 to about 15 mol percent of the polybutadiene units having the 1,2-addition configuration.
• the formulas for the block copolymers can be represented by the modified formulas S-B1-B2-B3 and (S-B1-B2-B3)nX respectively.
• each B1 and B2 is as defined hereinbefore.
• the peak molecular weight of the B3 block would range from about 1,000 to about 25,000 and the overall peak molecular weights of the block copolymers would be within the same range defined above. More specifically, the monovinylaromatic block will remain at 10,000 to 25,000 with the overall peak molecular weight of the three polybutadiene blocks being from about 25,000 to about 190,000 with the weight ratio of B1 to B2 remaining as defined above.
• the second of these embodiments comprises one or more block copolymers having at least one monovinylaromatic block and at least one polybutadiene block having a vinyl content that tapers from a vinyl content of less than 15 mol percent at the first end of the polybutadiene block adjacent to the monovinylaromatic block to a vinyl content that is greater than 25 mol percent at the second end of the polybutadiene block which is furthest from the monovinylaromatic block.
• the block copolymer compositions of this embodiment utilized in the present invention will comprise:
• S is a monovinylaromatic hydrocarbon block having a peak molecular weight from about 10,000 to about 25,000
• B4 is a polybutadiene block having a vinyl content that tapers from less than 15 mol percent at the first end adjacent to the monovinylaromatic block (S) to a vinyl content that is greater than 25 mol percent at the second end which is furthest from the monovinylaromatic block (S) and wherein the S-B4 block copolymer has a peak molecular weight from about 40,000 to about 200,000;
• each S is a monovinylaromatic hydrocarbon block having a peak molecular weight from about 10,000 to about 25,000 and each B4 is a polybutadiene block having a vinyl content that tapers from less than 15 mol percent at the first end adjacent to the monovinylaromatic block (S) to a vinyl content that is greater than 25 mol percent at the second end which is furthest from the monovinylaromatic block (S), n is an integer from 2 to 6, and X is the residue of a coupling agent and wherein the (S-B4) n X block copolymer has a peak molecular weight that is from 1.5 to 6.0 times the peak molecular weight of the S-B4 block copolymer; and
• the block copolymers of this embodiment may also further comprise an additional polybutadiene block (B5) having a vinyl content that is less than 15 mol percent.
• B5 additional polybutadiene block
• the formulas for the block copolymers can be represented by the modified formulas S-B4-B5 and (S-B4-B5)nX respectively.
• each B4 is as defined hereinbefore.
• the peak molecular weight of the B5 block would range from about 1,000 to about 25,000 and the overall peak molecular weights of the block copolymers would be within the same range as defined above.
• the monovinylaromatic hydrocarbon blocks (S) in the above noted formulas S-B4 or (S-B4)nX are as defined above, including the peak molecular weights.
• the polybutadiene of the B4 blocks of the above-noted formulas is polybutadiene monomer that is a substantially pure monomer or contains minor proportions, up to 10% by weight, of structurally related conjugated dienes. Preferably the polybutadiene is pure.
• Each block copolymer of the formula S-B4 utilized in the process of the present invention will have a peak molecular weight from about 40,000 to about 200,000, preferably from about 65,000 to about 160,000, even more preferably from about 75,000 to about 150,000.
• the peak molecular weight of the coupled block copolymers of the formula ( ⁇ -B4)nX is dependent upon the peak molecular weight of the block copolymer of the formula S-B4 utilized. More specifically, the peak molecular weight of the (S-B4)nX block copolymers will range from about 1.5 to about 6.0 times the peak molecular weight of the S-B4 block copolymer. Preferably, the peak molecular weight of the (S-B4)nX block copolymers will range from about 1.8 to about 5.0 times the peak molecular weight of the S-B4 block copolymer.
• the vinyl content taper or increase through the polybutadiene block such that the vinyl content ranges from less than 15 mol percent vinyl content (1,2-addition configuration) at the first end of the block adjacent to the monovinylaromatic block (S) to a vinyl content that is greater than 25 mol percent at the second end which is furthest from the monovinylaromatic block (S).
• the term “tapers” refers to the distribution of the 1,2-addition within the polybutadiene block B4 such that one end of the block (the end adjacent to the monovinylaromatic block) has a lesser degree of 1,2-addition ( ⁇ 15 mol percent) compared to the opposite end of the polybutadiene block which has a higher degree of 1,2-addition (>25 mol percent).
• the polybutadiene block is generally considered to progressively increase in 1,2-addition across the expanse of the block.
• the block may include small segments of “groupings” of vinyl groups of low vinyl followed by small segments of “groupings” of vinyl groups of higher vinyl.
• the overall effect though is that the vinyl content increase across the expanse of the block. In other words, the vinyl content would start at an amount less than 15 mol percent and would on average progressively increase throughout the block to an amount greater than 25 mol percent.
• the vinyl content at the first end of the block would range from about 7 to about 15 mol percent of the polybutadiene units having 1,2-addition configuration and would on average increase throughout the block such that at least the last 10% to 49% of the block, preferably 25% to 49% of the block has a vinyl content in which greater than 25 mol percent of the condensed polybutadiene units have a 1,2-addition configuration, preferably from about 25 mol percent to about 80 mol percent, more preferably from about 40 mol percent to about 75 mol, and even more preferably from about 50 to about 65 mol percent of the polybutadiene units in this segment have a 1,2-addition configuration.
• the monovinylaromatic hydrocarbon content of the copolymers is suitably from about 10 to about 40% by weight, based on the total block copolymer.
• the content of monovinylaromatic hydrocarbon of the copolymers will be from about 18 to about 35% by weight, more preferably from about 19 to about 32% by weight, based on the total weight of the copolymer.
• the block copolymer composition comprises a block copolymer of the formula S-B4 alone wherein S is a monovinylaromatic hydrocarbon block and B4 is a polybutadiene block having a vinyl content that tapers from less than 15 mol percent at the first end adjacent to the monovinylaromatic block (S) to a vinyl content that is greater than 25 mol percent at the second end which is furthest from the monovinylaromatic block (S).
• S-B4 may be used in combination with a coupled block copolymer of the formula ( ⁇ -B4)nX wherein each S is a monovinylaromatic hydrocarbon block and each B4 is a polybutadiene block having a vinyl content that tapers from less than 15 mol percent at the first end adjacent to the monovinylaromatic block (S) to a vinyl content that is greater than 25 mol percent at the second end which is furthest from the monovinylaromatic block (S), n is an integer from 2 to 6 and X is the residue of a coupling agent.
• n will be an integer ranging from 2 to 6.
• n will be an integer from 2 to 4, with 2 being the most preferred. While hydrogenation of block copolymers is well known in the art, the block copolymers of the present invention are in substantially unhydrogenated form.
• the ratio of the S-B4 block copolymer to (S-B4)nX block copolymer will be greater than about 1:1, preferably equal to or greater than about 3:2. In a particularly preferred embodiment, the ratio will be from about 3:2 to about 10:1 with the most preferred ratio being from about 4:1 to about 7:3.
• the block copolymer composition comprises a mixture of S-B4 and (S-B4)nX
• coupled polymer will always be present in an amount less than that of the S-B4 block copolymer (e.g., the coupled block copolymer will be present in the composition in an amount of at most 49.9% by weight, preferably at most 40% by weight).
• block copolymer compositions selected from block copolymer compositions that comprise:
• the block copolymer compositions utilized in the process of the present invention may be prepared by any method known in the art including the well known full sequential polymerization method, optionally in combination with reinitiation, and the coupling method, as illustrated in e.g. U.S. Pat. No. 3,231,635; U.S. Pat. No. 3,251,905; U.S. Pat. No. 3,390,207; U.S. Pat. No. 3,598,887, U.S. Pat. No. 4,219,627, EP 0413294 A2, EP 0387671 B1, EP 0636654 A1 and WO 94/22931, each incorporated herein by reference in their entirety.
• the block copolymers of the formula S-B1-B2 may be prepared via sequential polymerization wherein a polystyrene block is polymerized in step 1 , followed by the addition of a low vinyl polybutadiene block and then a high vinyl polybutadiene block.
• the low vinyl polybutadiene block the butadiene will be polymerized in the absence of a vinyl modifier.
• the high vinyl polybutadiene block the polymerization will occur in the presence of a vinyl modifier with the vinyl modifier being added all at once, concurrently or nearly concurrently, along with the additional dose of butadiene.
• the polystyrene block is polymerized in step 1 , followed by the addition butadiene in step 2 and then the gradual addition of a vinyl modifier in step 3 .
• the block copolymers prepared via sequential polymerization may also serve as intermediate living block copolymers (S-B1-B2 or S-B4), which are subsequently coupled by means of a multivalent coupling agent, the initial block copolymer S-B1-B2 or S-B4 content being determined by the coupling efficiency.
• a coupling efficiency in the range of from 80% to 97% is desirable.
• polymers having a coupling efficiency of up to 50% When coupling efficiency is above 50%, processing viscosities become higher than desirable.
• the coupling efficiency is in the range of from 10% to 30%, and still more preferred the coupling efficiency is in the range of from 10% to 20%.
• the coupling efficiency is preferably no less than 10%.
• the phrase “coupling efficiency” refers to the number of molecules of coupled polymer divided by the number of molecules of coupled polymer plus the number of molecules of uncoupled polymer. For example, if a coupling efficiency is 80 percent, then the polymer will contain 20 percent diblock. This is well known to those of ordinary skill in the art.
• the block copolymers may therefore, for example, be prepared by coupling at least two S-B1-B2 block copolymer molecules together or coupling at least two S-B4 block copolymer molecules.
• the coupling agent may be any di- or polyfunctional coupling agent known in the art, for example, dibromoethane, diethyl adipate, divinylbenzene, dimethyldichlorosilane, methyl dichlorosilane, silicon tetrachloride and alkoxy silanes (U.S. Pat. No. 3,244,664, U.S. Pat. No. 3,692,874, U.S. Pat. No. 4,076,915, U.S. Pat. No. 5,075,377, U.S. Pat.
• the polymers useful in the process of the present invention may be prepared by contacting the monomer or monomers with an organoalkali metal compound in a suitable solvent at a temperature within from about ⁇ 150° C. to about 300° C., preferably at a temperature within the range of from about 0° C. to about 100° C.
• organolithium compounds having the general formula RLi wherein R is an aliphatic, cycloaliphatic, alkyl-substituted cycloaliphatic, aromatic or alkyl-substituted aromatic hydrocarbon radical having from 1 to 20 carbon atoms of which sec butyl is preferred.
• Suitable solvents include those useful in the solution polymerization of the polymer and include aliphatic, cycloaliphatic, alkyl-substituted cycloaliphatic, aromatic and alkyl-substituted aromatic hydrocarbons, ethers and mixtures thereof.
• suitable solvents include aliphatic hydrocarbons such as butane, pentane, hexane and heptane, cycloaliphatic hydrocarbons such as cyclopentane, cyclohexane and cycloheptane, alkyl-substituted cycloaliphatic hydrocarbons such as methylcyclohexane and methylcycloheptane, aromatic hydrocarbons such as benzene and the alkyl-substituted hydrocarbons such as toluene and xylene, and ethers such as tetrahydrofuran, diethylether and di-n-butyl ether.
• Preferred solvents are cyclopentane or cyclohexane.
• polar compounds such as ethers, amines and other Lewis bases and more in particular those selected from the group consisting of dialkylethers of glycols.
• Most preferred modifiers are selected from dialkyl ether of ethylene glycol containing the same or different terminal alkoxy groups and optionally bearing an alkyl substituent on the ethylene radical, such as monoglyme, diglyme, diethoxyethane, 1,2-diethoxypropane, 1-ethoxy-2,2-tert-butoxyethane, of which 1,2-diethoxypropane is most preferred.
• the first dose of butadiene is added without the addition of modifier and allowed to polymerize to form B1.
• additional butadiene is added along with a sufficient quantity of the modifier to achieve a second polybutadiene block (B2) having a higher vinyl content.
• the modifier may be added all at once in order to produce a second butadiene block that has a fairly consistent vinyl content throughout the block or the modifier may be gradually added in order to produce a second polybutadiene block that is somewhat tapered (with the vinyl content gradually increasing throughout the block).
• the butadiene is added to the reaction vessel and then the modifier to be used is gradually added in a controlled manner in order to give the tapered vinyl content.
• the amount of modifier utilized will depend on the exact modifier being used. In general, the modifier will be added in an amount from about 50 to about 5000 parts per million basis solvent.
• bitumen component and block copolymer compositions may be added during the process of the present invention, including, but not limited to, resins, oils, stabilizers, anti-statics, fillers (such as talc, calcium carbonate and carbon black), polyphosphoric acid, ground tire rubber or flame retardants.
• the amount of such optional ingredients added can range from 0 to about 20% by weight, based on the total weight of the bituminous binder composition.
• Particularly preferred additional ingredients are antioxidants which may be added during or after the mixing process to affect the rate of reaction. When antioxidants are added, they are present in an amount from about 0.1% by weight to about 5% by weight, based on the total weight of the bituminous binder composition.
• block copolymers may also be included in the final bituminous binder composition of the present invention.
• block copolymers will be block copolymers of the general formulas C-D-C or (C-D)nX wherein C is a monovinylaromatic hydrocarbon block and D is a conjugated diene block, n is an integer from 2 to 6 and X is the residue of a coupling agent, said block copolymer having a peak molecular weight from about 30,000 to about 400,000 and a vinyl content from about 8 mol percent to about 25 mol percent based on the number of repeat monomer units in the conjugated diene block of the block copolymer.
• block copolymers examples include, but are not limited to, Kraton D1101 polymer and Kraton D 1184 polymer, each commercially available from Kraton Polymers LLC.
• additional block copolymers When such additional block copolymers are present, they will preferably be present in an amount up to about 30% by weight, based on the total weight of block copolymer added.
• these additional components When these additional components are added to the process, they are typically added at the same time as the block copolymer composition. Alternatively, these additional components may be added just before the addition of the block copolymer composition or just after the addition of the block copolymer composition.
• the present invention further relates to a specific polymer modified bituminous binder composition that is substantially free of any cross-linking agents, said bituminous binder composition comprising:
• the present invention still further relates to a specific bituminous binder concentrate that is substantially free of any cross-linking agents, said bituminous binder concentrate comprising:
• the present invention is particularly suited for hot mix bitumen concrete, the products of the present invention will also be useful in other typical SBS polymer modified bitumen paving applications such as hot chip seals, and cut backs. It is also envisioned that the present invention is suitable for non-paving applications such as modified bitumen roll roofing, self-adhesion waterproofing membranes, sound deadening and vibration damping compounds. The present invention is also useful for recycled asphalt pavement.
• bitumens were used in the examples below. Those skilled in the art are aware that many bitumens can be modified to varying degrees with conventional SBS polymers while others are moderately to extremely difficult to modify. Two bitumens which are generally considered to be “difficult” bitumens were utilized to demonstrate the present invention. More specifically, the European bitumen utilized can typically be modified with SBS polymers but requires sulfur or other crosslinking technology for suitable compatibility. The West Texas bitumen utilized is incompatible to the degree that it typically cannot be modified with SBS polymers at all.
• Comparative Polymer C1 s a low vinyl, low molecular weight, low diblock content polymer in pellet form, commercially available from Kraton Polymers LLC as Kraton D1102 polymer.
• Comparative Polymer C2 is a medium vinyl, high coupled styrene-butadiene-styrene block copolymer in porous pellet form.
• Comparative Polymer C3 is a high vinyl, low coupled styrene-butadiene-styrene block copolymer in porous pellet form as described in U.S. patent application Ser. No. 11/598,511.
• Comparative Polymer C4 is a low vinyl, high coupled styrene-butadiene-styrene block copolymer in porous pellet form, commercially available from Kraton Polymers LLC as Kraton D1101 polymer.
• Comparative Polymer C5 is a low vinyl, high coupled styrene-butadiene-styrene block copolymer in porous pellet form, previously commercially produced by Kraton Polymers LLC as Kraton D1144 polymer (no longer commercially available).
• Comparative Polymer C6 is a high vinyl, high coupled styrene-butadiene-styrene block copolymer in porous pellet form, commercially available from Kraton Polymers LLC as Kraton D1192 polymer.
• Comparative Polymer C7 is a 4-arm radial version of Comparative Polymer C3 comprising 29% 4-arm radial polymer and 71% residual diblock (prepared as noted below).
• Comparative Polymer C8 is a 4-arm radial version of Comparative Polymer C3 comprising 43% 4-arm radial polymer and 57% residual diblock (prepared as noted below). Comparative Polymer C7
• the first portion was terminated with 3.0 mL of methanol and allowed to stand for 10 minutes. After cooling down the reaction mixture, 0.2% BHT was added for stabilization. The portion was then blended to produce a polymer with 28.6% coupling efficiency. The product was isolated by steam stripping to give white crumbs.
• Comparative Polymer C7 was utilized in the preparation of Comparative Polymer C8 with the following exceptions: 0.46 mL of the coupling agent GPTS was then added to the second portion of the reaction mixture. The reaction mixture was allowed to stand for 28 minutes at 70° C. then terminated with 1.5 mL of methanol. After cooling down the reaction mixture, 0.2% BHT was added for stabilization. The portion was then blended to produce a polymer having 43.0% coupling efficiency. The product was isolated by steam stripping to give white crumbs.
• Inventive polymers 1, 2 and 3 of the present invention were prepared by conventional polymerization methods based on the general procedures noted below:
• Table 3 lists the molecular parameters obtained for Inventive Polymers 1, 2 and 3.
• the vinyl content of the second polybutadiene block B2 was calculated based on the measured vinyl content of the first polybutadiene block B1, the measured vinyl content of the whole polymer, and the relative molecular weights of polybutadiene blocks B1 and B2. ***Estimated, not measured.
• the ductility test is a measure of the distance to which a bituminous material will elongate before breaking when two ends of a briquette specimen of the material are pulled apart at a specified speed and at a specified temperature. The test was performed at a temperature of 5° C. ⁇ 0.5° C. and with a separation speed of 5 cm/min ⁇ 5.0%. Certain samples were tested for Softening Point Roll and Ball according to ASTM D36, rotational viscosity according to ASTM D4402 and Separation for Storage Stability according to ASTM D5892. Certain samples were also tested for Elastic Recovery according to ASTM D6084. These tests are commonly used to evaluate Polymer Modified Bitumens and are well known to those skilled in the art.
• Example 5 is exemplary of the present invention and Examples 1 to 4 are comparative examples.
• the ductility of Example 5 is substantially higher, both at 5° C. and 25° C., than that of the other Examples, while all five Examples exhibit adequate elastic recovery and softening point.
• Table 5 below compares Inventive Polymer 1 as set forth in Example 5 above with differing times and temperatures. Examples 5 to 9 indicate the optimum processing time and temperature of the present invention. Processing at 190° C. gives both the optimum ductility and elastic recovery. The shorter low shear processing time of 6 hours also improves both ductility and elastic recovery.
• Examples 10 to 13 demonstrate that the Inventive Polymer of Example 8 above at optimum conditions outperforms other Comparative Polymers at the optimum conditions.
• Examples 14 to 16 demonstrate the improved compatibility of the Inventive Polymer compared to a standard linear styrene-butadiene-styrene copolymer.
• Examples 17 to 21 demonstrate the scope of molecular parameters of the present invention.
• Examples 17 and 18 are attempts to increase ductility by adding radial character to a polymer. These examples show that this approach is not effective.
• Example 19 shows that a low vinyl/high vinyl block structure with a higher polybutadiene molecular weight still gives excellent ductility, but the higher molecular weight will also give higher viscosity which is not desirable.
• Example 20 shows that reducing the polybutadiene molecular weight causes a significant reduction in ductility.
• Examples 22 to 28 demonstrate the effectiveness of the polymers of the present invention in meeting a stringent specification in an incompatible bitumen.
• the Inventive Polymer in Examples 24 and 25 show a superior combination of high softening point, good ductility, good elastic recovery and low Fraass temperature.

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